3.0 Ultrasonic Treatment Technology Description

How it works

Ultrasonic liquid treatment uses high frequency energy to cause vibration in liquids to produce physical or chemical effects. Ultrasound, part of the sonic spectrum that ranges from 20 kHz to 10 MHz, is generated by a transducer that converts mechanical or electrical energy into high frequency acoustical (sound) energy. The sound energy is then fed to a horn that transmits the energy as high frequency vibrations to the liquid being processed. A typical ultrasonic processing chamber is shown in Figure 3-1.

When liquids are exposed to these high frequency vibrations, both physical and chemical changes occur as a result of a physical phenomenon, known as cavitation. Cavitation is the formation, expansion, and implosion of microscopic gas bubbles in liquid as the molecules in the liquid absorb ultrasonic energy. Compression and rarefaction waves rapidly move through the liquid media. If the waves are sufficiently intense they will break the attractive forces in the existing molecules and create gas bubbles. As additional ultrasound energy enters the liquid, the gas bubbles grow until they reach a critical size. On reaching a critical size, the gas bubbles implode or collapse (Figure 3-2).

The energy that exists within the cavity and in the immediate vicinity of the gas bubbles just before collapse causes both physical and chemical effects in the liquid. Physical effects result when cavitation is intense enough to rupture cell membranes, free particulates from solid surfaces, and destroy particles and organisms through particulate collisions or by forcing them apart. Chemical effects result because the conditions immediately proceeding collapse of a cavitation bubble are similar in magnitude to ultra-high energy combustion conditions. Within the cavitation bubble and the immediate surrounding area, temperatures range from 2000 to 5000E C, and pressure reaches 1800 atmospheres. These extreme temperatures and pressures, which last only microseconds, do not exist long enough to heat the liquids being processed. However, the localized temperature and pressure increases are sufficient to increase chemical reactivity, polymer degradation, and chemical free-radical production (IES, 1998).

Technology Applications

Because of the physical and chemical effects of the vibratory energy on liquid media, ultrasonic techniques are used in the processing of liquids for numerous applications. Current applications include emulsification, dispersion, disruption of biological cells, removal of trapped gases, cleaning of microscopic contamination, and acceleration of chemical reactions.

Applications in the waste-treatment and environmental fields have emerged only within the last few years as the technology been researched for its efficiency, effectiveness, and scale-up potential for large-volume treatment applications. Recent and current research for environmental applications focus on the use of ultrasound for the treatment and destruction of pathogens in wastewater, intake-pipe anti-fouling (particularly zebra mussels and Asiatic clams), and as a fish deterrent to reduce entrainment.

Figure 3-1

BalsurvUSFig2.jpg (56522 bytes)

 

Figure 3-2

 

BalsurvUSFig3.jpg (27679 bytes)Battelle’s survey of vendors in the ultrasonic industry revealed that traditional ultrasound technology is currently applied to the processing of low volumes and flow rates, typically in the range of 60-100 gpm. Many of the contacted vendors were uncertain that the technology could be scaled up to handle the flows necessary to treat ballast water in a full-size commercial vessel.

The one technology that shows promise for economical and efficient scale up uses a high-energy ultrasonic system. This system, referred to as High Power Ultrasonic Process (HPUP), delivers energy vibrations into the liquid at a much greater intensity than conventional systems. Compared to other systems, HPUP produces more intense cavitation. Thus, necessary exposure time for mortality or destruction of biological organisms is reduced, and high flow rates of the treated liquid are possible. Table 3-3 shows the operating requirements and specifications for a 600-gpm HPUP system, composed of six treatment chambers, each with the capacity flows of 100 gpm.

The HPUP system that would be applicable to treatment contains six 100-gpm cylinders set in a circular configuration (Figure 3-3), allowing one treatment unit the capability to treat a flow of 600 gpm. Therefore, two treatment units would be needed to treat the specified 1,200 gpm flows and 13 units would be necessary to treat a scaled up flow of 8,000 gpm. Since the diameter of one 600gpm system is three feet, space requirements become the limiting factor of this treatment option especially at scaled up flow levels. Distances and positioning among the treatment units and generator tower can be variable. However, the threshold of distance among treatment units has not been determined.

Table 3-1. HPUP Ultrasonic System Equipment
General Operating Specifications for 50 - 600 GPM Systems
1

Equipment Weight

Sub-unit Dimensions

  • Treatment Unit
  • Generator Tower
Variable

Example dimensions for the 6-chamber, 600-gpm system shown in Figure 3-3:

  • 36 inches diameter ´ 54-60 inches high (91 ´ 137-152.4 cm)
  • 72 ´ 24 ´ 18 inches (183 ´ 61 ´ 45.7 cm) (height/length/width)
Energy Requirements
  • 40 kW/hr (1,000 gpm) to 294 kW/hr (7,350 gpm)
Connections/Fittings/ Equipment Room/ Environment
  • Intake diameters: 6 – 8 inches (15 – 20 cm)
  • Maximum intake pressure: 70 PSI is acceptable, but best known performance when intake pressure is <50 PSI
  • Temperature is not a limit for this technology
Operation Concerns
  • Maintenance
  • Environmental
  • Safety
  • Minimal, if any, maintenance required.
  • Systems should operate 12,000+ hrs without any maintenance
  • No known environmental concerns
  • High temperatures generated in the transducer necessitate circulation of cooling water to keep the transducer from overheating.
Filtration Effects

· Biological

· Operational

  • Filtration will increase performance by removing organisms that have higher resistance to the treatment. Correspondingly, however, filtration may decrease effectiveness on smaller organisms by removing particulate matter that would increase kills through collision.
  • Filtration is unnecessary for optimal operational performance.
Performance Issues
  • Essentially no moving parts (friction surfaces).
  • Performance will not degrade over time.
  • Operational performance is known to be optimal at intake pressures of 50 PSI. However, the effects of pressures above this limit are unknown.
Equipment Capital Purchase Cost

 

  • It is estimated that each 600-gpm unit would cost $250,000.
  • Price per unit expected to decrease with a multiple-unit purchase
  • Excludes installation
1 The equipment flow rates presented in this table are variable because of modular design. Additional modules will increase flow rates in a linear progression, limited only by available space and energy requirements.

One of the parameters that influence the operational performance of ultrasound treatment is intake pressure. IES reports that pressures of 50 PSI are optimal for their 600-gpm model. However, they have not tested the effects of intake pressure at 70 PSI on optimal performance. It is their opinion it will not have much impact on operational and biological performance. Tests must be performed on the system to evaluate the effects of the increased pressure.

Potential Space-Saving Alternative for Ultrasonic Equipment

IES, the HPUP vendor, suggested that one way to conserve shipboard space would be to submerge the treatment units into the ballast tanks, as their units are completely immersible. With ballast-system configurations on most commercial vessels, it is difficult to conceptualize how submerging the treatment chambers in the ballast tanks can be used to save shipboard space—problems with installing, servicing, and monitoring the operation of in-tank treatment units appear to offset the space-saving benefits (and IES admits this, as they are unfamiliar with ship design and operation). However, submerging all or some of the ultrasonic treatment units may be feasible for newly constructed vessels, and potentially possible for some ballast tanks on retrofitted vessels. The cost/benefit of submerging treatment units as a means to conserve space and scale up flow rates of treated water should be further assessed by a naval architect if this novel means to conserve ship space is further considered.

In all ultrasonic equipment, mechanical or electrical energy is transformed to ultrasound by a transducer. At the scale-up sizes necessary for commercial-ship applications, the energy conversion transducer will heat to very high temperatures and therefore requires a separate cooling system. This requires that a small amount of ambient temperature water be available to circulate around the transducer during operation. The current IES HPUP system cannot use saltwater primarily because of the percent solids. However, modifying the cooling designs to use seawater appears possible, especially if the treatment units were submerged in the ballast tanks.

Ultrasound Treatment Performance

Biological Effects

The primary means for biological eradication are the mechanical effects rather than chemical reactions that result from cavitation. Cell membranes and organisms are literally ruptured or blown apart from the intense energy created. The primary mechanisms of microorganism death are attributable to the physical effects associated with cavitation. These effects include:

  • Completed destruction or death of microorganisms and larger biota, and
  • Disturbance or rupture of biological cell membranes, leading to subsequent organism death. (See depiction of cell rupture in Figure 3-4).

Reported Treatment EffectivenessBalsurvUSFig4.jpg (26489 bytes)

Though specific research has not been conducted for the treatment of ballast water, ultrasonic technology has been researched for other shipboard applications. A 1970s study on treatment of shipboard wastewater demonstrated that effective cavitation could not be attained for the volumes of water being treated (NRC, 1996). Consequently, sufficient sterilization of the wastewater was not achieved. Traditional methods of ultrasonic treatments are reviewed in Stemming the Tide (NRC, 1996) which states that effectiveness is variable when treatment is applied to higher organisms such as zebra mussel veligers and fish. NRC concluded however, that such ultrasound systems could destroy fungi, yeasts, and pathogenic bacteria.

The vendor survey conducted under this study revealed that most current operating ultrasonic systems are used for small-scale flow applications (i.e., <100gpm). Only IES has developed and researched ultrasonic systems for applications and flow rates comparable to what is needed for commercial ship ballast-water treatment.

IES has researched ultrasonic effectiveness on microorganisms (both viral and bacterial) and larger organisms such as zebra mussels and Asiatic clams. Although IES has developed and installed 600-gpm systems for research purposes, and achieved good results, they have not installed a system for commercial use. The data presented in Table 3-2 represents information received by the IES for a 100 gpm-flow unit processing unfiltered water.

Table 3-2. Treatment Effectiveness for Various Organism Sizes and Type

Organism Type Size Performance
Zebra Mussel Veligers Mollusk 70 microns 100% mortality1
Poliovirus Virus < 5 microns 7 log10 reduction
Heliminth ova, Ascaris Nematode 8-10 microns 100% inactivation
Cryptosporidium parvum Bacteria ~ 5 microns 6 - 7 log10 reduction
Data source: Innovative Environmental Solutions, Inc. Advance, NC
1 100% mortality of zebra mussel veligers has also been demonstrated in 600gpm-flow systems

In summary, a wide range of organism size is effectively treated with ultrasonic technology. One-hundred percent kill or inactivation is achieved in larger organisms and 99.9999 - 99.99999% (6log to 7log) reduction is achieved in bacterial and viral communities. Bacteria and viral community recolonization under ballast-tank conditions following a 6log – 7log reduction has not been studied.

IES has no HPUP mortality data on potential nuisance species, such as Gymnodinium dinoflagellate cysts. However, HPUP and other ultrasonic treatments have demonstrated that sufficient energy and conditions are present to break zebra mussel shells. It is therefore speculated that ultrasonic treatment technology is capable of killing dinoflagellate cysts, one of the hardiest forms of biota in ballast tanks. Relatively simple laboratory tests would be necessary to test this hypothesis.

Filtration Effects

The biological effectiveness of ultrasonic technology will be enhanced to a certain degree by high level filtration to screen larger organisms. However, one of the primary mechanisms of organism mortality using ultrasonic technology is destruction or damage due to collisions within the liquid. Therefore, biological effectiveness is expected to increase with the amount of particulates in the water (O’Dette, 1998). Thus, a balance must be determined between the exclusion (by filtration) of the hardier larger organisms and the retention of some particulate matter to enhance the mortality of microorganisms in the ultrasonic treatment chamber.

Operational performance is not affected by prefiltration. Since the energy level in the processing chamber is high enough to keep particulate matter from settling, any particles introduced into the chamber during ballasting will be flushed out with the continual flow of ballast water being treated.

In summary, no determination can made be about the four pretreatment scenarios of 250-m m, 100-m m, 25-m m, and no filtration, nor to the expected biological effectiveness of current ultrasonic technology applied to ballast water.

Robustness

In general, ultrasonic treatment systems (including the IES HPUP system) will be extremely resistant to typical shipboard conditions. There are no parts with friction surfaces to wear out. Since all parts of the system are fabricated or covered with stainless steel, equipment corrosion from saltwater is not a concern even if the systems are to be submerged in the ballast tanks. The generator tower, which would be more susceptible to adverse conditions, can be located in a different area than the treatment chambers.

Other conditions that the system maybe exposed to are high air temperatures, vibrations, rolling and pitching, and fumes. None of these will affect the efficiency or long term operation of the equipment.

Ease Of Operation

The IES HPUP system discussed previously is relatively simple to operate. The system, requires operator input only at the generator tower. This input involves setting the controls at an initial setting and rechecking the controls when the unit is powered on. Some training is necessary to understand the control settings. Additional operational checks need to be performed on the system to ensure that the cooling water is circulating around the transducer.

Very little maintenance is required on the system and IES reports that their system can run for up to 12,000 hours before any maintenance is required. When maintenance is required, it involves approximately 2 hours of labor time to clean each unit of sediment residuals.

Safety

There are several ultrasonic safety concerns that should be addressed relative to shipboard application of this technology. The first issue is the use of high voltage (220 V) electricity to power the system. Considering that other shipboard machinery runs on high voltage (220 and 440V) this should not be a major factor assuming that shipboard safety requirements for high voltage electricity will to be adhered to during the installation process.

Heat build up in the transducer is the other safety concern. In the IES HPUP system, the transducer requires a circulating water-cooling unit whenever it is in operation. If the cooling system is operating properly, there should be no reason for safety concerns. All heated metal parts are out of contact and housed within the cooling unit. If, however, the transducer’s cooling system does not work properly, the transducer could overheat and fail. Risk from burning or explosions of the transducer are considered extremely remote.

Environmental Concerns

There are no additives introduced into the ultrasonic system and no by-products generated by ultrasonic technology. Therefore, there are no anticipated environmental concerns associated with this technology.

Operation and Maintenance (O&M) Costs

The O&M costs associated with the IES HPUP system are minimal, with the exception of energy costs. Energy consumption for operation of the HPUP system is shown in Table 3-3. As stated previously, about two hours of cleaning maintenance is required every 12,000 hours of operation (for each 100-gpm-treatment chamber)

Table 3-3. Summary of HPUP Operation Costs


Water Flow Treated (gpm)


Power Consumption (kW)


Cost of Power
(cents/kWh)

Cost of Power Consumption
($/month)1

1,000

28

3

605

7,350

206

3

4,450

30,000

840

3

18,144

SOURCE: Innovative Environmental Solutions, Inc. Advance, NC
1 Cost of power consumption is based on 24-hour/day operation.

01 April 2001
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